Apparatus for treating fruit



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APPARATUS" FOR TREATING FRUIT Original Filed July 31, 1940 I 4 Sheets-Sheet 4 g Q 15 M'VZW E 454514526624? the parent application.

Patented Sept. 11, 1945 APPARATUS FOR TREATING FRUIT Ogden S. Sells and Howard L. Porch, Riverside, CaliL, assignors to Food Machinery Corporation, San Jose, Calif a corporation of Dela- Y ware Original application July 31, 194i), Serial No. 348,978. Divided and this application July 5,

1943, Serial No. 493.538

11 Claims.

This invention relates to the art oi. treating fresh whole fruit with the principal object of reducing the shrinkage of fruit treated thereby and enhancing the appearance thereof.

The present application is a division of applicants co-pending application for U. S. Letters Patent Serial No. 348,978, filed July 31,1940; on Method for treating fruit, which issued February 15, 1944, as Patent No. 2,342,063. The present case covers the apparatus originally disclosed in The method of the invention constitutes an improvement on that particular method of treatin fruit set forth in U. S. Letters Patent of Jagen N. Sharma 2,212,621.

The Sharrna method aforesaid involves the application in diffused condition of a clear solution of wax in a highly volatile solvent toiresh fruit and the like, in relatively small quantities so that the fruit will not be burned thereby, and then permitting the solution so applied to be undisturbed to cause the evaporation of' solvent from the particles of solution on the fruit so that the wax in these particles of solution is deposited in situ on the fruit. The object of the Sharma process is to control the shrinkage of the fruit treated so the-tit will remain in fresh condition longer thanotherwise, and to give the fruit a bright, fresh appearance.

In the early stagesof development'of the Shara ma process, the wax solution was applied to the fruit by an ordinary paint spray gun in which the.

difiusion of the solution was produced by propelling from the nozzle a pencil-like stream of the solution and impacting converging jets of air travelling at high velocity against the stream oi solution. These air iets'broke the solution up into fine particles and formed these particles into a I fan-shaped blast of mist which was propelled, by the force of the stream' of liquid and the jets of air, over a distance of three or four feet into contact with a layer of fruit to be treated.

Performing the Sharma method in this manner I produced satisfactory shrinkage control of the fruit without damaging the latter but the cost was high. It was very much desired, therefore, to decrease the cost of the process if there was any way that this could be done.

One of the expensive features of performing the Shanna method with paint spray guns was the cost of the guns themselves and the air compressing apparatus necessary to operate these. In treating fruit with the Sharma process, with an average size applicator of four-foot width, two such guns were necessary, and the cost of these guns was about twenty dollars each. The air compressor needed to supply these guns with air cost in the neighborhood of three hundred dol-- lars. To cheapen his method, Shanna substituted spray nozzles operated by hydraulic pressure for the paint spray guns, as these nozzles could be bought for less than two dollars each and a pump to deliver the solution to these nozzles can be had for approximately five dollars.

In his patent, above identified, Sharma discloses the manner in which he uses hydraulic nozzles for treating fresh fruit with a solution of wax. Sharma found it necessary, however, to use four nozzles in the average size applicator of four-foot width. The amount of solution required by the Shanna method disclosed in said patent still made this a relatively expensive process and it is an ob- Ject of the present invention to provide an apparatus for treating fresh whole fruit with a solution of waxy material for retarding the shrinkage and improving the appearance of said fruit which has a relatively high efilciency from the stand point of the amount of material used.

Ject as wellas other objects and-advantages will be made manifest in the following description taken in connection with the accompanying drawings, in which:

Fig. 1 is a perspective view of a preferred embodiment of the apparatus of this invention with portions of the housing thereof broken away to disclose certain of the operating elements of the apparatus.

Fig. 2 is a cross-sectional view of said apparatus taken on the line 2-2 of Fig. 1.

Fig. 3 is a cross-sectional view taken on the line 3-3 of Fig. 2.

Fig. 4 is an enlarged fragmentary cross-sectiona1 view taken on the line 4-4 oi Fig. 3.

Fig. 5 is a still further enlarged detail cross-sec-= tional view taken on the line 55 of Fig. 4.

Fig. 6 is a diagrammatic view taken on the same plane as Fig. 4 and illustrating the spinner drive of said apparatus.

'and i9 respectively, the wall l3 providing a receiving delivery plate 20 at the bottom of the opening l8, while the wall l6 provides a discharge plate 2| at the bottom of the opening I 9. Extending into the intake opening I8 is a central baffle plate 22 and side baiile plates 22 as seen in Figs. 2 and 3, these plates restricting the intake of air through the inlet opening id in a manner described hereinafter. Partially closing the fruit outlet opening i9 is a flexible curtain 23 formed by horizontal metal strips 24 flexibly joined at adjacent edges thereof as seen in Fig. 2. The apparatus i is shown as positioned in between a drier 25 which is adapted to receive fruit F to be processed, and a conveyor 26 onto which fruit is discharged upon its leaving the apparatus iii.

The lower portion 27 of the housing wall it extends outwardly for a reason which will be made clear hereinafter. Provided in the housing i2 so that one end thereof is closed by the wall It and so as to extend through the wall it, is a cylindrical exhaust pipe 3@. An upper forward sector is cut away to provide an opening 35, from the lower edge of which a drip pan 32 extends as shown in Figs 2, whilefrom the upper edge of said opening a short wall 33 extends upwardly and rearwardly.

Mounted in the housing 92 is a roller conveyor 45. This conveyor includes an endless series of rollers il which are rotatably mounted on chains d2 which are trained about suitable sprockets fixed on shafts it, t1, and 8, opposite ends of which are journalled in suitable bearings in the housing walls id and it. The path of the conveyor M3 is triangular as shown in Fig. 2 and surrounds the exhaust pipe 30. The upper flight of the conveyor is inclined upwardly from the point at which it receives fruit from the delivery plate 20 toward the point where it discharges this fruit onto the discharge plate 2!. The conveyor 40 is driven from the shaft it by a sprocket it fixed on this shaft and a chain Ell which connects this sprocket with a pinion on a shaft 52. One end of the latter shaft is journalled in a bearing mounted on the lower portion 2? of the wall it. The other end of this shaft is connected by a suitable flexible coupling (not shown) to the gear shaft E3 oi a geared motor 55 which is mounted on the base frame it just outside the wall it.

As shown in Fig. 3, the rollers :38 are preferably provided with metal straps 56 helically wound about these rollers and secured thereto, the straps on adjacent rollers being pitched in opposite directions. Upper flights of the chains 62 travel on tracks 58 which are mounted on inner surfaces of the walls it and it. Also mounted on and extending inwardly from these walls are guard aprons 85, the lower edges of which turn downwardly and extend close to the ends of the cylindrical outer surfaces of the rollers d l Each of the rollers 6!, at the end thereof adjacent the wall it, is provided with a sprocket 66. These sprockets of the rollers in the upper flight or the conveyor come into mesh with a spinner chain Bi which rides on a track 68 and is driven as shown in Fig. 6 by a chain and sprocket connection with the shaft 41 so that the upper flight of the chain e'i travels in the opposite direction from the upper flights of the chains 82. .The spinner chain 67! thus causes the rollers M to spin relatively rapidly while they are in the upper flight of the conveyor Gt, the direction or rotation of the rollers being such as to cause the uppermost surfaces of these rollers to travel toward the discharge end of the conveyor at a velocity which is several times that of the bodily movement of the rollers with the chains 42.

Connecting the tracks 58 on opposite sides of essence the machine is a spreader bar 10 (see Fig. 2) which-not only rigidly spaces the tracks 58 and assists in supporting the track 68, but it also provides a support for a bafiie plate ll, straps 12 of which are shaped to support this baflle plate partiallyon the spreader bar 10 and partially on the drip pan 32.

It is to be noted that a good-sized air space is left open between the upper edge of the .bafiie plate H and the wall 33 and a somewhat smaller air space is left open between the lower edge of the bafile plate ll and the drip pan 3:2.

Mounted on theopen end of the exhaust pipe 36 is an air evacuating blower having a fan 76 which is rotated by V-belts Ti directly driven by a triple drive pulley it of the motor 55. The fan is is mounted so that when rotated it exhausts air from the exhaust pipe 39 and discharges this air upwardly through a pipe 88 which preferably leads to a point outside the building in which the apparatus It is installed, the purpose for this being made clear hereinafter. The inner of the three runways of the drive pulley 118 receives a 'belt 8| .by which a solution pump 82 is driven by the motor 55. When the pump 82 is being driven by the motor 55,11, sucks treating solution up from a storage tank (not shown) through a pipe 33 after passing this through a filter 8 3, and then delivers this solution through. a pipe' 86a and a pressure control system S to a pipe 85 which leads to the spray mechanism 90 of the apparatus ill. This mechanism is mounted on an inverted U-shaped frame M which is secured to the outside. of walls 5 and I5 and extends upwardly above the cover H.

The mechanism so includes a channel mounting plate 92 which is flxedupon the U-shaped frame at, this channel member carrying a fan motor -93 and having secured to opposite ends thereof a spray unit at. These spray units being substantiallyjdentical, a description of one will suflice for both. Each of the units 95 includes a fanhousing 95 which surrounds a fan 98, the latter being mounted upon one of a pair of drive shafts 91 extending in opposite directions from the motor at. The'fan housing 95 has a relatively large discharge opening 95 which fits into the upper end of a conduit housing not. This housing provides a central conduit HM, an upper conduit Hi2, and a lower conduit m8. Mounted in "each of the housings Hit is a pipe H0, these being connected together by a pipe Ill, and supplied with solution by the pipe 85. Each of the pipes H6 supports and supplies solution to a nozzle H2 which is held by its mounting on said pipe i ill with its axis coinciding with that of the conduit illl as shown in Fig. 4 and with the tip end of the nozzle substantially in the plane of the discharge mouth of said conduit ml. As shown in Fig. 5, each nozzle H2 is of the hydraulic pressure spray type I from which the solution fed thereto is sprayed in a cone of spray I 93.

The optimum conditions produced in the apparatus of this invention have been attained when using for the nozzles H2 what is commercially known as the Binks #40 nozzle which is illustrated in Fig. 5 and in which the discharge aperture is of a diameter of 1/64 of'an inch or less. Various nozzles have been tried out in which the angle of the cone of spray varies from 45 degrees up to degrees. The smaller angle in the cone of spray, however, has resulted in a relatively narrow distribution bi the solution in the operation of the apparatus and it has been found that an angle of from 80 to 90 degrees in the cone of spray glvesthe optimum spread and consequently the highest degree of emciency.

this is about 2.25 square inches.

The system 8 functions to control the pressure with which solution is delivered by the pump 82 through the pipe to the spray mechanism 00. This system include a valve I It, a pressure regulator H5, a solution. return pipe Ill which leads back to the solution tank (not shown) and a pressure g e I, all of which are connected together and with the pipes a and 85 as shown in Fig. 1.

Operation ture with sperm'acetti wax, paraflln of various grades and of different melting points being thus used, the type selected depending upon the atmospheric conditions and the temperatures under which the process is performed Other waxy materials which may be utilized in the process and apparatus of the present invention include beeswax, ozocerite, and hydrogenated edible oils.

Various volatile solvents may be employed including petroleum solvents such as lacquer diluents, rubber solvent, and refined petroleum distillates. The essential characteristic of the solvent employed is that it should be sufficiently In this formula, 7% of wax is employed for 93% of solvent. The war: is In paraflin with a melting point of F. and /1 spermacetti USP. The solvent in this formula goes, commercially by the term Rubber Solvent A'and is made by the Shell Oil Company, Inc., of California. It has a boiling point range of 160 F. to 230 F. This solution is applied in performing the process of our invention under 20 pounds pressure, with the nozzles adjusted to dispense. one gallon per hour per nozzle on a flow of fruit through the ma- .chine at the rate of pounds per nozzl per minute. That is,-one gallon of the solution is used for treating four and one-half tons of fruit.

As already indicated, the apparatus I0 is adapted to operate in conjunction with and in line between a drier 25 and a conveyor belt 26, so as to receive fruit F from the drier and after waxing this fruit, to then discharge said fruit,to the conveyor 26. The apparatus I0 is set in operation by energizing the motors 55 and 93. The motor 55 runs the conveyor 40 in the manner abovedescribed so as to receive any fruit delivered onto the upper flight of the rollers 4| from the delivery plate 20 and carry this fruit in a slightly inclined layer while rotating the individual pieces of fruit until the fruit is discharged from the conveyor onto the discharge plate 2|. The motor 55 also rotates the exhaust blower 16 at high speed so as to suck air downwardly through open portions of the opening 3| in the exhaust pipe 30, this air passing through the exhaust. fan 16 and being discharged upwardly through the pipe 80. In order to reach the exhaust pipe 30, the air thus sucked thereinto must pass into the apparatus l0 through the intake and discharge volatile to evaporate readily in the process. For

example, in the treatment of citrus fruit by this process a rubber solvent may be employed having a boiling point range of 140 F. to F. In cases where the atmospheric temperatures met with are somewhat lower, solvent has been employed having a boiling point range of 100 F. to 210 F. Where the atmospherictemperature is very high, lacquer solvents having boiling point ranges of 160 F. to 270 F. and F. to 350 F. have been found suitable.

Generally. and particularly for the treatment of citrus fruits, the end boiling point of the volatile solvent employed should be below about 350 F. and it ispreferred to employ solvents the boiling point ranges of which are between 100 F. and 350 F., or at least 90% to 95% of the solvent should hav a boiling point below about 350 F.

The waxy material should be substantially completely dissolved in the volatile solvent so as to avoid clogging the nozzles. Generally speaking,

the amount of wax which can be held in solution varies with the temperature of the solution. In cases of extremely high atmospheric temperatureopenings l0 and I9, and downwardly through the upper flight of the conveyor 40 from the space thereabove. Most of the air thus drawn into the apparatus I0 enters through the intake [8 rather than through the discharge H! as the latter is substantially restricted by the curtain 23. As will be seen in Fig. 3, the baffle plates 22 and 22' restrict all of the upper half of the intake l8 except for areas adjacent opposite sides of the spray units 94 and similar areas adjacent the side walls I and IS. The purpose of exhausting this air from just below the conveyor 40 is to dispose of all solvent vapors produced in the waxing process and thus prevent contamination of the air in the packing house in which the apparatus i0 is installed. At the same time, this exhausting of the air from the housing prevents an explosive mixture of air and solvent vapor from developing therein.

The motor 55 also runs the pump 82 and :builds up pressure against the valve H4 through which solution must pass from the pump 82 to the pipe 85. The valve H4 is kept closed until fruit is actually travelling through the apparatus l0. When this is the case, the pump 82 produces such a pressure of solution against the valve I H as to force this solution. through the pressure regulator Hi into the overflow pipe H8 and thence .back to the storage tank from which the pipe 83 leads. when fruit is travelling through the machine and a suitable pressure of solution has been built up by the pump 82 as indicated by the pressure gauge 1, the valve. I H is opened and the solumotor 93 causes the fans 95 to suck air into the housings 95 and discharge this air downwardly through the conduit housings Ito and out through the conduits itl, I02, and it. This air is preferably discharged through these conduits at a velocity of from two to three thousand feet per minute. The cross-sectional area of the conduits llli, Hi2 and it, being as above stated, preferably about two square inches each, the jets of air delivered from these conduits travel at an extremely low rate compared with paint gun practice. The object of this is to prevent fur ther breaking up the particles of solution delivered in'the spray cones Hi3 into the path of these jets of air. These converging jets, however, serve to take up the particles of solution delivered thereto in the cones H8 and spread these out in' two fan-shaped streams entirely across the conveyor id.

The optimum velocity of the jets aforesaid is 2450 feet per minute and the velocity of the air in the stream formed thereby where this contacts the fruit carried on the conveyer Gil varies from 200. to 550 ieetper minute. Under these optimum conditions the jet velocity is within a. range of about 12.6 times one of the velocities with which said stream contacts the fruit. The average velocity at which the major portion of said air stream contacts said fruit is preferably The op-' between 450 and 500 feet per minute. I timum jet velocity is thus within a range of approximately five times said average.

It should be understood that the particular apparatus disclosed and optimum values above mentioned are illustrative only and that the present invention is capable of being practiced with a wide variety of specific types of apparatus and velocity ratios. It is to be noted however that there is a marked contrast between the illustrative velocity ratios given and the corresponding velocity, ratios of current paint spray gun practice which are of an extremely'higher order.

In ordinary paint spray gun practice, it is common to surround a jet of the liquid to be sprayed with a sleeve of air travelling at a very high rate of speed so as to cause an instantaneous dispersion of the liquid in the form of a blast of very fine fog. Where it is desirable in paint gun practice to flatten out this blast of fog in applying it to a surface, the blast is hit shortly after it is formed by converging jets of air travelling at terrific speed.

In the present invention, the central column of air passing through the conduit It! does not have the effect of dispersing the sprayed liquid into fine particles. It merely feeds into the columns of air emitted from the conduits I02 andlilt, to aid in the formation of a fan-like stream of air moving approximately along the axis of the nozzle H2 directly and rapidly toward the fruit carried on the conveyer. The central column of air also performs the useful function of preventing particles of solution being driven back onto the nozzle H2 which would tend to clog the nozzle with an accumulation of wax.

The cone of spray H3 is formed entirely by hydraulic pressure. It is not produced partly by hydraulic pressure and partly by air pressure as is the case with the central jet of spray initially produced in paint spray gun practice. A noz'zle for forming a spray entirely by hydraulic pressure comes under the term film forming" nozzle which is applied to all nozzleswhich disessence a solid medium. This class of nozzles are represented by four common types of construction: (a) the common pressure nozzle in which the liquid issuing from an orifice is given a whirling motion and thereby forms a widening conical film of spray; (b) the impinging nozzle in which a jet of liquid at high velocity strikes a surface or edge and spreads into a fan-shaped spray; (c) the double-jet nozzle in which two jets of liquid impinge, forming a fiat fan-shaped spray similar to type b; and (d) the spinning cup or disc spray in which a sheet of liquid is thrown from a rapidly revolving edge by centrifugal action.

The nozzles commonly used in paint spray gun practice and previously described are classified commercially under the term atomizing nozzles. In these the liquid that is sprayed is delivered to the nozzle at a relatively low pressure and is torn into threads or filaments by a high velocity jet of compressed air or steam. (Page 1376, vol. 30, No; 12, Industrial and Engineering Chemistry, issued December, 1938.)

The present invention was developed after the foremost manufacturers of paint spray guns in America had been given an opportunity to solve the problem of effectively applying a volatile solution of wax to fruit, and had failed to accomplish this with a degree of emciency making it practical. The reason for their failure is now attributed to the fact that the spray gunlwhich had the best results of all those which they tried had an air jet nozzle velocity of 171,400 feet per minute, these jets coming from major orifices which were of an inch in diameter and having -mist, or fog, and flattened out this fog into a highlyv turbulent blast of flattened cross-section. This might be very good practice for handling paints and it might seem to be very good practice for the purpose of waxing fresh fruits with highly volatile solution of wax, yet it turned out, after the present invention was discovered, to be relatively inefficient for the latter purpose.

Various explanations might be made of the exceptional efiiciency in waxing fruit obtained by the present invention over paint gun practice, the most acceptable theory advanced being as follows:

The process and apparatus of this invention diffuses the solution without breaking this up anywhere near so finely as is inevitable in paint spray gun practice. The relatively large drops of solution thus produced are dispersed and adequately conveyed by a fiat, rapidly moving stream of air which delivers these particles to the surfaces of the fruit with a relatively slight loss of solvent from the solution while the particles are in transit as compared with the loss in handling this solution by paint spray gun practice.

The efiiciency of the present invention also exceeds that of the apparatus shown in the Sharma patent aforesaid in which the currents of air deperse liquid in spray form by the application of mechanical energy directly to the liquid thro solution onto the fruit are set up entirely by the sucking of air downwardly through the fruit-carrying conveyor. In the present invention, air is not only evacuated downwardly through this conveyor, but the solution sprayed into the atmosphere by the hydraulic pressure with which it is delivered to the nozzles is entrained in relatively large particles in a rapidly moving fan-propelled stream of air formed by-jets of exceedingly large cross-sectional area and delivered at comparatively very small muzzle velocity. Thus, the rel-' apparatus. It is thought that the secret of this emclency is to be found in the diminished opportunity for evaporation of the solvent from the solution when applied in accordance with the present invention. The larger particles expose much smaller surface area to evaporation for a given volume of solution than the finer particles. Then rapidly conveying these particles, as in the present invention, from the point of their formation to their contact with the fruit, without further dividing said particles, subjects these particles to contact with the air for a relatively brief interval as compared with the Sharma apparatus.

This explanation is based on the reasoning that, being much more fluid upon its reaching the fruit in the present invention, the solution spreads over a greater area for a given quantity of solution; and that the amount of shrinkage control obtained is proportional to the area over which the solution spreads, rather than to the precise amount of solution deposited on the fruit.

We claim:

1. In an apparatus for applying a very light liquid in finely divided condition to individual objects such as pieces of fruit, the combination of: a hydraulic spray nozzle; means for supplying said liquid to said nozzle under a hydraulic pressure sumcient to cause said liquid to be discharged from said nozzle in a cone of spray particles;

means for conveying a layer of said objects past said nozzle; a relatively low power air fan; housing means for receiving air discharged from said fan; and conduit means receiving relatively large volumes of air from said housing means and discharging said air against said cone of spray particles and towards said objects so as to form a rapidly moving stream of air in which said particles are entrained'and rapidly conveyed into.

contact with said objects with a relativelyshort period of exposure to evaporation.

2. In an apparatus for applying a very light liquid in finely divided condition to individual objects such as pieces of fruit, the combination of; a hydraulic spray nozzle; means for supplying said liquid to said nozzle under ahydraullc pressure sufficient to cause said liquid to be discharged from said nozzle in a cone of spray particles; a relatively low power air fan; housing means for receiving air discharged from said fan and said air causing said stream to entrain and convey said liquid particles as, aforesaid without the impact of said lets against said particles producing a substantial further subdivision of said particles. 1

'3. In an apparatus for applying a very light liquid in finely divided condition to individual obiects such as pieces of fruit, the combination of:

a, hydraulic spray nozzle; meansfor supplying said liquid to said nozzle under a hydraulic pressure suflicient to cause said liquid to be discharged from said nozzle in a cone of spray particles; a

relatively low power air fan; housing means for receiving air discharged from said fan and forming this into jets which converge from above and below to form a fan-shaped stream of air travelling rapidly towards and into contact with said fruit, the liquid particles formed in said cone of spray being entrained in said stream and delivered thereby onto said fruit so rapidly as toallow a relatively limited amount of evaporation from said. particles during their travel in said air stream, the relatively large volume of air contained in said jets as compared with the relatively low pressure applied by said fan in propelling said air causing said stream to entrain and convey said liquid particles as aforesaid without the impact of said lets against said particles producing a substantial further subdivision of said particles; and conduit means surrounding said nozzle and receiving air from said housing, the

air so received forming a column flowing around and past said nozzle and enveloping said cone of spray to carry the particles thereof into said converging iets.

4. A spraying apparatus comprising: an air conducting casing having a plurality of discharge ports arranged in angular relation to discharge converging currents of air; means for causing a flow of air at a relatively low pressure diflerential through said casing and out of said ports; a liquid spray nozzle arranged behind and directed toward the point of convergence of said air currents; and means for supplying liquid to said nozzie under sufficient pressure to discharge it therefrom in the form of a spray.

5. A spraying apparatus comprising: an air conducting casing having a plurality of discharge ports arranged in angular relation to discharge converging currents of air; means for causing a flow of air through said casing and out of said ports; a liquid spray nozzle arranged and directed toward the point of convergence of said air currents; and means for supplying liquid to said nozzle under sufllcient pressure to discharge it therefrom in the form of a spray of particles, the cross sectional area of said ports being extremely large in contrast with that of the discharge orifice of said spray nozzle whereby said ports under a relatively low pressure differential discharge relatively large volumes of air in said currents, the latter uniting as they converge to form a stream of air traveling rapidly away from said spray nozzle, the particles of liquid formed by said spray n'ozzle being entrained in said stream of air and rapidly conveyed onto a surface to be sprayed therewith.

6. A spraying apparatus comprising: an air conducting casing having a plurality of discharge ports arranged in angular relation to discharge converging currents of-air; means for causing a flow of air through said casing and out of said ports; a liquid spray nozzle arranged behind and directed toward the point of convergence of said air currents; and means for supplying liquid to said nozzle under suflicient pressure to discharge it' therefrom in the form of a spray of particles,

the cross sectional area of said parts being extremely large in contrast with that of the discharge orifice of said spray nozzlewhereby said ports, under a low pressure difierential, discharge relatively large volumes of air in said currents, the latter uniting as they converge to form a stream of air travelling. rapidly away'from said spray nozzle, the particles of liquid formed by said spray nozzle being entrained in said stream of air and rapidly conveyed onto a surface to be sprayed therewith, said means for causing air to flow through said casing producing such a low pressure differential between the atmosphere and the interior of said casing that the air in said currents travels at insumcient velocity for the impact of said currents against said spray particles to produce a substantial further subdivision of said particles.

7 A spraying apparatus comprising: an air conducting casing having a plurality of outer discharge ports arranged in angular relation to discharge currents of air along converging axes, and an intermediate discharge port arranged to discharge an air current toward the point of convergence of the others; means for causing a flow of air through said casing and out said ports, a liquid atomizing nozzle disposed in said intermediate port; means for supplying liquid to said nozzle under sufilcient pressure to discharge it therefrom in the form of dispersed particles, the

' cross sectional area of said ports being extremely to discharge such relatively large volumes of air through said ports at as relatively low a velocity and pressure as are suificient to entrain and rapidly carry away the aforesaid dispersed liquid particles without substantially reducing their fineness. .l

8. In a spray apparatus adapted for the spraying of a light liquid, the combination of: means for forming spray particles by applying mechanical energy directly to said liquid through a solid medium th'ereby dispersing said particles into the atmosphere; an air housing having relatively large openings pointed towards said particles close to where said particles are formed; means for supplying air under a relatively low pressure differential to said housing, said openings being. relatively large so that air supplied to said housing as aforesaid flows outwardly through said openings against said spray particles with sufficient volume to entrain and rapidly carry said particles along a given path against an object to be sprayed with said liquid the velocity of said currents being insuflicient tocause the impact of said air against said particles to effect a substantial degree of further subdivision of said particles.

9. An apparatus for delivering a volatile liquid into the atmosphere and uniformly applying the same to surfaces to be treated therewith without permitting a substantial degree of evaporation of said liquid while the latteris travelling said air being impelled as aforesaid under a relatively low pressure difierential whereby the impact of said air with said particles is insumoient to produce a substantial degree of further subdivision of said particles.

10. An apparatus for dispersing a highly volatile liquid through the atmosphere to uniformly apply said liquid to a layer of fruit with a minimum amount of evaporation of said liquid while so dispersed, said apparatus comprising: a hydraulic spray nozzle having a relatively small orifice and adapted to spray said liquid into the atmosphere to divide said liquid into relatively coarse particles; means for supplying said liquid to said nozzle under hydraulic pressure to cause said nozzle to produce a spray as aforesaid; an air fan; and means for receiving air propelled by said fan and directing said air against said spray in jets which are extremely large in cross section as compared to the orifice of said spray nozzle thereby forming a stream of air entraining said particles and conveying them relatively rapidly into contact with said fruit, the rapidity of said stream resulting from the relatively large volumes of air impacting against said spray in said air jets, the velocity of said impact however being so low as to prevent said impact causing more than an inconsiderable amount of further subdivision of said hydraulically generated spray particles.

11. An apparatus for dispersing a highly volatile liquid through the atmosphere to uniformly apply said liquid to a layer of fruit with a minimum amount of evaporation of said liquid while so dispersed, said apparatu comprising: a hydraulic spray nozzle having a relatively small orifice and adapted to spray said liquid into the atmosphere to divide said liquid into relatively coarse particles; means for supplying said liquid to said nozzle under hydraulic pressure to cause said nozzle to produce a spray as aforesaid; an air fan; and means for receiving air propelled by said fan and'directing said air against said spray in converging jets which are extremely large in cross section as compared to the orifice of said spray nozzle thereby forming a fan-shaped stream of air entraining said particles and conveying them relatively rapidly into contact with said fruit, the rapidity of said stream resulting from the relatively large volumes of air impacting against said spray in said air jets, the velocity of said impact however being so low as to prevent through the atmosphere, said apparatus com rising: means for delivering said liquid under a substantial super-atmospheric hydraulic pressure to a point of dispersal spaced a substantial dis-.

said impact causing more than an inconsiderable amount of further subdivision of said hydraulically generated spray particles.

OGDEN S. SELLS. HOWARD L. PORCH.

cnm'mxcau or commoner. I Potent No. 258149792. September 11, i9l .5.

oenxn s. 811313,!!! AL;

It is hereby certified that error appears in the printed specification of the ebove numbered pate t requiring correction as follows: Page i first oolumn, ,line 11;; name of ,petentee, for "Jegen" read-' -Jegah; page 5, seeond oo1umn,'1i .ne. 51, after "arranged" insert --beh1nd--; end that the said letters Patent should be read with this correction therein that .the some may conform to the record of the casein the Patent Office.

Signed and sealed this 18th day of December, AID. 1914.5.

Leslie Frazer (Seal) First Assistant Commissioner of Patents. 

